WO2009065577A1 - Centrale électrique modulaire, indépendante du réseau - Google Patents

Centrale électrique modulaire, indépendante du réseau Download PDF

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Publication number
WO2009065577A1
WO2009065577A1 PCT/EP2008/009803 EP2008009803W WO2009065577A1 WO 2009065577 A1 WO2009065577 A1 WO 2009065577A1 EP 2008009803 W EP2008009803 W EP 2008009803W WO 2009065577 A1 WO2009065577 A1 WO 2009065577A1
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WIPO (PCT)
Prior art keywords
plant
power plant
synthesis
methanol
desorption
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PCT/EP2008/009803
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German (de)
English (en)
Inventor
Gregor Waldstein
Original Assignee
Gregor Waldstein
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Gregor Waldstein filed Critical Gregor Waldstein
Priority to US12/744,104 priority Critical patent/US8715581B2/en
Priority to AT08851992T priority patent/ATE537358T1/de
Priority to EP08851992A priority patent/EP2220367B1/fr
Publication of WO2009065577A1 publication Critical patent/WO2009065577A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/1516—Multisteps
    • C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03D—WIND MOTORS
    • F03D9/00—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations
    • F03D9/007—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations the wind motor being combined with means for converting solar radiation into useful energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03D—WIND MOTORS
    • F03D9/00—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations
    • F03D9/10—Combinations of wind motors with apparatus storing energy
    • F03D9/19—Combinations of wind motors with apparatus storing energy storing chemical energy, e.g. using electrolysis
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03D—WIND MOTORS
    • F03D9/00—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations
    • F03D9/20—Wind motors characterised by the driven apparatus
    • F03D9/25—Wind motors characterised by the driven apparatus the apparatus being an electrical generator
    • F03D9/255—Wind motors characterised by the driven apparatus the apparatus being an electrical generator connected to electrical distribution networks; Arrangements therefor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S20/00—Solar heat collectors specially adapted for particular uses or environments
    • F24S20/70—Waterborne solar heat collector modules
    • H—ELECTRICITY
    • H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
    • H02S—GENERATION OF ELECTRIC POWER BY CONVERSION OF INFRARED RADIATION, VISIBLE LIGHT OR ULTRAVIOLET LIGHT, e.g. USING PHOTOVOLTAIC [PV] MODULES
    • H02S10/00—PV power plants; Combinations of PV energy systems with other systems for the generation of electric power
    • H02S10/10—PV power plants; Combinations of PV energy systems with other systems for the generation of electric power including a supplementary source of electric power, e.g. hybrid diesel-PV energy systems
    • H02S10/12—Hybrid wind-PV energy systems
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/30—Alkali metal compounds
    • B01D2251/304—Alkali metal compounds of sodium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/30—Alkali metal compounds
    • B01D2251/306—Alkali metal compounds of potassium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/40—Alkaline earth metal or magnesium compounds
    • B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/602—Oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/604—Hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/40—Further details for adsorption processes and devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77—Liquid phase processes
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465—Composition of the impurity
    • C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
    • F05B2210/00—Working fluid
    • F05B2210/16—Air or water being indistinctly used as working fluid, i.e. the machine can work equally with air or water without any modification
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
    • F05B2210/00—Working fluid
    • F05B2210/18—Air and water being simultaneously used as working fluid
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y02A20/138—Water desalination using renewable energy
    • Y02A20/141—Wind power
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y02A20/138—Water desalination using renewable energy
    • Y02A20/142—Solar thermal; Photovoltaics
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/20—Capture or disposal of greenhouse gases of methane
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/30—Energy from the sea, e.g. using wave energy or salinity gradient
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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    • Y02E10/47—Mountings or tracking
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/50—Photovoltaic [PV] energy
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/70—Wind energy
    • Y02E10/72—Wind turbines with rotation axis in wind direction
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/32—Hydrogen storage
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E70/00—Other energy conversion or management systems reducing GHG emissions
    • Y02E70/30—Systems combining energy storage with energy generation of non-fossil origin
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    • Y02P20/133—Renewable energy sources, e.g. sunlight
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    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Definitions

  • the invention relates to a power plant connected to power, which generates and stores from CO2 of the air, water and regenerative energy, combustible hydrocarbons, this power plant is preferably installed on a float; Furthermore, the use of such a power plant and method for operating such a power plant.
  • a further disadvantage of the known methods is that storage media for electrical energy have a low energy density; furthermore, renewable energy can often be generated cheaply in places and / or at times where the need for it is low.
  • liquid fuels in particular hydrocarbons
  • methanol should be mentioned as a particularly advantageous source of energy; in particular, since it is the simplest hydrocarbon-containing compound which is liquid at room temperature.
  • methane is a cheap source of energy, since there is a strong infrastructure for this KW to the end user.
  • Hardy et al., US 2005/02328833 also disclose a process for recovering fuels (hydrocarbons) comprising the steps of alkaline CO2 absorption, C02 release, H2 electrowinning, methanol synthesis from H2 and CO2 components and conversion to hydrocarbons by Fischer-Tropsch synthesis , This document proposes to cover the required energy with a nuclear reactor.
  • An essential purpose of the entire plant disclosed therein is to produce directly on board a ship hydrocarbons for use as fuel.
  • the invention thus relates to a power plant without power for the production and storage of combustible hydrocarbons, in particular methanol, dimethyl ether and methane.
  • the invention further relates to a process for the production of combustible hydrocarbons, a floating body equipped with a power plant as described herein and the use of the power plant or the floating body for the production of combustible hydrocarbons fe.
  • the term power plant generally refers to a network of different power plants. In the narrower sense, such composite systems are called, which generate electrical energy and deliver it to an existing network. In the context of the present The invention is intended to describe the term but also those plant compounds which provide a chemical energy source (in particular methanol, methane, dimethyl ether). Such a power plant is unbetztebun- the if it has no direct connection to a consumer, but the generated energy (or the energy source) stores and thus provides for delivery.
  • a chemical energy source in particular methanol, methane, dimethyl ether
  • a floating body generally refers to any device capable of receiving the plant components mentioned below and being able to float in regions of constant wind conditions / wave motion.
  • this term includes all types of vessels that can move on their own (“mobile floats”, eg by motor power, “motor vessels” or wind power, “sailing ships") or must be moved ("stationary floats”, eg “pontoons”
  • the term "floats moved by wind power” includes not only classic ships equipped with mast and sail but also unconventional sailing ships which use, for example, a sail kite or other technical equipment.
  • floats may be constructed as monohull or multihull boats.
  • methanol synthesis or “methanol production” refers to the formation of methanol from hydrogen and carbon dioxide or carbon monoxide.
  • methanol production refers to the formation of methanol from hydrogen and carbon dioxide or carbon monoxide.
  • the required hydrogen can also be formed in situ, resulting in the following gross equation:
  • DME dimethyl ether
  • the chemical energy carriers (methanol, DME, methane) formed according to these reactions can be present in different purities and do not have to be generated completely chemically pure, i. By-products, impurities from the previous reaction steps and / or the starting material, etc. may be included.
  • the chemical energy source provided according to the invention is suitable, if appropriate after further purification steps, to be used as an energy carrier in internal combustion engines or fuel cells or as a starting material in chemical syntheses. The invention is further illustrated by the figures.
  • Fig. 1 shows a schematic representation of a power plant according to the invention wherein the reference numerals have the following meaning: Aggregates
  • FIG. 2 shows a schematic representation of a floating body according to the invention comprising a power plant for the production of methanol, wherein the reference signs have the following meaning:
  • Fig. 3 shows a particular embodiment of the wind turbine, in which the wind turbine and the CO2 absorption system are combined with each other by the rotor blades of WICA are provided with microporous membranes for CO 2 absorption.
  • 1 shows the low-carbon flow and 2 the CO 2 -rich return of the wash liquor.
  • the invention relates to a power plant without power, characterized in that it contains the following, in their capacity coordinated systems ("modules"): a) wind turbine, hydropower plant, solar thermal system and / or photovoltaic system for generating electrical energy for the operation of plants b) to f) b) C02 absorption plant for the absorption of atmospheric CO2 c) CO2 desorption plant for the desorption of CO2 obtained in b) d) electrochemical or solar thermal H2 synthesis plant for the operation of the plant e); e) synthesis plant selected from the group of catalytic methanol synthesis, catalytic DME synthesis, catalytic methane synthesis; f) storage facility selected from the group methanol storage facility, DME storage facility, methane storage facility.
  • modules in their capacity coordinated systems
  • Such a power plant offers the possibility of harvesting and storing the energy present in wind power, hydropower and / or solar energy almost independently of location. This opens up a great potential for possible locations.
  • the chemical energy source that is, the storage medium methanol, DME, methane
  • Methanol is an energy source with a comparatively high energy density, which is easy to handle and can be stored for a long time. Further, the methanol formed according to the present invention can be easily integrated into the existing power supply systems, used as a chemical raw material, or directly used in fuel cells (e.g., in DMFC cells). DME and methane are also energy sources with comparatively high energy density, which are easy to handle and storable. Furthermore, the chemical energy carriers formed according to the invention can be easily integrated into the existing energy supply systems, used as a chemical raw material, or used directly in fuel cells.
  • the invention relates to the special tuning of the synthesis technology to the performance of the wind power, hydropower and / or photovoltaic plant; the functional integration of components of the synthesis plant in the wind power hydropower and / or photovoltaic system; the specific selection and design of the individual plants.
  • the systems a) to f) can also be designed as combined systems. So the wind turbine (a) by special design, the function of the C02 absorption system (b) partially or completely take over. Furthermore, the electrochemical H2 synthesis plant (d) and the catalytic methanol synthesis plant (e) can be combined, for example in the form of an inverted Direct Methanol Fuel Cell (DMFC). Furthermore, the C02 desorption unit (c) and the electrochemical H2 synthesis unit (d) can be combined with each other. Also, the C02 absorption and desorption can be combined or functionally coupled. Such combined or combined systems are included in the present invention.
  • DMFC Direct Methanol Fuel Cell
  • a thermal CO 2 desorption plant with a solar thermal H2 synthesis plant.
  • a CO 2 desorption plant which works on the principle of reductive alkaline low-pressure electrolysis with a methanol synthesis plant based on synthesis gas.
  • the following modules can be combined with each other as desired.
  • Float The term has already been explained at the beginning. Floats can be created specifically for the purpose of the invention. Alternatively, existing equipment can be reused, for example by equipping freighters or rigs with the appropriate equipment. Suitable floats include cargo ships and buoys.
  • Plant for the production of energy (module a): depending on the configuration, electrical and / or thermal energy is required for the process described here. This energy is provided via a primary plant. In principle, all known systems are suitable which provide electrical or thermal energy. Wind turbines, hydropower plants, photovoltaic systems and solar thermal systems should be mentioned as advantageous installations, with wind turbines and solar thermal systems being particularly noteworthy. Furthermore, hydropower plants deserve special mention.
  • WKA wind turbines
  • module al By wind turbines (“WKA”), (module al) are meant in the context of the present invention, all systems that can convert wind energy into electrical energy .
  • WKAs contain a rotor hub and rotor blades, which is mounted on a mast and with The term thus includes WKAs with vertically or horizontally rotating rotor blades, and WKAs may be used with or without transmission assistance.
  • module a2 Under hydropower plant (module a2) are in the context of the present invention, all facilities to understand that either harness the kinetic energy of the water or make the relative movement of float to water available. Preference would therefore also be a moving float ("sailing ship") which moves through substantially dormant water becomes. Also preferred is a floating body, which can convert the energy of the water waves into electrical energy.
  • module a4 Under solar thermal system (module a4) are in the context of the present invention, all systems to understand that make the radiation energy of the sun thermally usable.
  • modules are known per se and commercially available or designed and manufactured according to known methods.
  • a vertically rotating wind turbine is used without gear support.
  • This embodiment has the advantage that a particularly low-maintenance WKA and easily mountable WKA is used.
  • a horizontally rotating power plant with gearbox support is used.
  • This embodiment has the advantage that a particularly energy-efficient and flexible WKA is used.
  • a solar thermal system and possibly a WKA is used.
  • This embodiment is advantageous when the following systems show a low demand for electrical energy and a high demand for thermal energy.
  • a wave force machine eg of the "Pelamis” or “OPT Powerbuoy” type
  • Such wave power machines are either anchored or positioned by other means, for example via sails.
  • a sailboat with attached OPT Powerbuoys is thus a specific embodiment of the above-mentioned hydropower plant.
  • an in-water turbine is used (e.g., as used in tidal power plants) which utilizes a flow in the water, e.g., a sea current.
  • Such turbines can, for example, be attached to stationary floats.
  • the invention therefore also relates to a modular power plant in which the floating body is stationary and which has a turbine arranged in the water.
  • an in-water turbine is used, which is attached to the hull of a sailboat.
  • said sailboat is moved by wind power relative to the water and thus drives the turbine for power generation.
  • Said sailboat can be either a classic sailboat with one or more hulls, or a boat which is equipped with non-konvnetionellen facilities for wind propulsion, such as a kite.
  • the invention therefore also relates to a modular power plant in which the floating body is a sailboat which has one or more turbines arranged in the water.
  • CO2 absorption system module b
  • Numerous plants and processes for the absorption of atmospheric CO2 are known.
  • CO2 absorption plants comprise plants based on a wash liquor (wet chemical plants, module b1), or without the use of wash liquors ("dry chemical plants", b2).
  • a wash liquor in particular an alkaline aqueous solution, preferably an alkali hydroxide such as NaOH or KOH, where Carbonate and / or bicarbonate, see Weimer et al, Energy Convers. Mgmt. 1996, p.1351 ff, which is incorporated by reference in this description (in particular: Chapter 3.3.2).
  • a wash liquor in particular an alkaline aqueous solution, preferably an alkali hydroxide such as NaOH or KOH, where Carbonate and / or bicarbonate, see Weimer et al, Energy Convers. Mgmt. 1996, p.1351 ff, which is incorporated by reference in this description (in particular: Chapter 3.3.2).
  • the CO2 of 1700m3 of air is needed.
  • 120000m3 of air must be fed per hour to the absorption plant.
  • Suitable wash liquors react reversibly with CO2 and are generally known, by way of example mention may be made of the already mentioned NaOH solution.
  • the absorption may be in open contact in a padded scrubbing tower.
  • the air flow is possibly first moistened and then passed in countercurrent to the alkaline wash liquor through this equipped with packing absorption tower.
  • the absorption system is of the Venturi tower type.
  • Venturi towers of this kind contain means for supplying the aqueous alkaline solution, means for dropping / atomizing this solution in the upper area of the tower, means for removing the formed carbonate / bicarbonate solution in the lower area of the tower.
  • Suitable venturi towers are known from US 4339547, which is incorporated by reference into this specification (in particular: Fig. 3a, b, column 2, Z. 63 - Sp.3, Z. 38)
  • the absorption system contains microporous hollow fiber membranes, in particular hydrophobic microporous hollow fiber membranes, which contain alkaline absorption liquid and are brought into contact with an air stream so as to absorb atmospheric CO2.
  • microporous hollow fiber membranes in particular hydrophobic microporous hollow fiber membranes, which contain alkaline absorption liquid and are brought into contact with an air stream so as to absorb atmospheric CO2.
  • Such membranes are known and commercially available, for example, from Hoechst-Celanese.
  • the design and dimensioning of corresponding absorbers is known per se and, for example, in Stucki et al, Int. J. Hydrogen Energy, 1995, p. 653 et seq.
  • these microporous membranes are coated with a hydroscopic material, for example MgSO.sub.4, which reduces the evaporation of the circulating water the washing solution.
  • a hydroscopic material for example MgSO.sub.4
  • the wind turbine and the CO 2 absorption system are combined with each other by the rotor blades and / or the mast of the WKA are provided with the aforementioned microporous membranes.
  • These membranes are mounted on mast and / or rotor blade in such a way that on the one hand they are in direct contact with the air and on the other hand the wash liquor can circulate to and from the CO2 desorption plant.
  • the invention therefore also relates to wind power plants and power plants without power, as described here, in which the rotor blades and / or the mast are provided with hydrophobic microporous membranes for CO 2 absorption.
  • an evaporation-reducing component is added to the wash liquor.
  • Suitable components have a vapor pressure reducing effect.
  • Such components are known per se, as a specific example is called magnesium sulfate.
  • the effective concentration of such components depends on the design of the plant, the feedstock used and the operating conditions. The determination of suitable operating parameters can be determined on the basis of appropriate tests; as an indication, 0.1 to 10% by weight of MgSO4 in the wash liquor are suitable.
  • Module b2 In the context of the present invention, preference is also given to systems in which air is contacted with solid CaO at comparatively low temperatures (in particular ⁇ 100 ° C.), with formation of CaCO 3.
  • the said CaO is advantageously present in finely divided form, for example as nanoparticles.
  • Corresponding apparatuses and systems which absorb gases by means of a solid absorbent are known per se and can be designed according to known methods. This dry chemical plant is preferably combined with the dry chemical C02 desorption plant mentioned below.
  • CO2 Desorption Plant (Module c): Systems for releasing CO2 from wash liquors, in particular from carbonate-containing aqueous wash liquors, are generally known (module c1). Equipment for the release of CO2 from solids, in particular from carbonate-containing solids, are also generally known (module c2). Such release may be by physicochemical, electrochemical or chemical means and is closely related to the compounds formed by CO 2 absorption.
  • the CO2 release takes place electrochemically by electrolysis of the carbonate solution formed in an electrochemical membrane cell to form CO 2 and H 2 ("alkaline low-pressure electrolysis", module rapid)
  • electrolysis of the carbonate solution formed in an electrochemical membrane cell to form CO 2 and H 2
  • Such cells are known per se; Na2CO3 + 4H2O -> 3H2 + 3/202 + CO2 + 2NaOH
  • the advantage of this embodiment lies in the fact that the C02 desorption unit and the H2 synthesis unit are combined with one another.
  • the CO2 release takes place electrochemically by electrolysis of the carbonate solution formed in an electrochemical membrane cell to form CO (eg using a solid oxide electrolysis cell, SOEC, module cl2).
  • CO a solid oxide electrolysis cell
  • SOEC solid oxide electrolysis cell
  • the release of CO2 by chemical means by acidification of the wash liquor from Appendix b) with optionally subsequent electrodialysis module cl3.
  • the desorption by adding an acid eg. aqueous sulfuric acid
  • an acid eg. aqueous sulfuric acid
  • the salt formed in this reaction can be worked up again in a subsequent electrodialysis.
  • the reactions can be described by the following equations: Na2CO3 + H2SO4 -> Na2SO4 + CO2 + H2O Na2SO4 + H2O -> NaOH + H2SO4.
  • the advantage of this embodiment lies in the simple and safe CO 2 desorption.
  • the release of CO2 takes place on a physicochemical (thermal) path by calcination (module c2).
  • a (alkaline) Alkalicarbonat Favor calcium carbonate, so far heated that CO2 is split off.
  • Suitable reactors for this reaction are known, for example rotary kilns or fluidized bed reactors.
  • the required (alkaline) alkali metal carbonates can be obtained directly from the CO2 absorption plant (by wet chemical or dry chemical route) or by reaction with Na2CO3 (from the absorption plant).
  • the metal oxides formed in the calcination can be recycled by reaction with water (for wet chemical processes) or recycled without further chemical reaction (for dry chemical processes).
  • the reaction can of the wet-chemical process by the following equations, which summarize the provision of the carbonate, the calcination and the recycling: Na 2 CO 3 + Ca (OH) 2 -> CaCO 3 + 2NaOH
  • An advantage of this embodiment is that a particularly finely divided carbonate is provided for the further reaction sequence.
  • Another advantage of this embodiment is that electrical energy can be dispensed with to carry out the reaction.
  • the solids are present in finely divided form, preferably as nanoparticles.
  • Mo duls c2 C02 release from CaC03 carried solar thermally at 500 - 2000 0 C, preferably about 1000 0 C.
  • solar thermal plants are known; suitable in principle all such systems that produce by bundling or focusing the desired temperatures; For example by means of parabolic mirror or Fresnel lenses.
  • the partial pressure of CO2 can be lowered in the reaction space in order to favorably influence the release.
  • a reduction of the CO 2 partial pressure is, for example, possible by H2 introduced into the reaction space.
  • the release of CO2 by chemical means by reaction of the carbonate solution with chlorine ("desorption by chlorination", module cl4), optionally in the presence of a catalyst, to form a chloride / hypochlorite solution and CO2 Reaction and corresponding devices ("stripping towers”) are known per se.
  • the required chlorine is recycled electrochemically; For example, by the initially formed chloride / hypochlorite solution is reduced and then fed to the H2 synthesis plant in which a chlor-alkali electrolysis is carried out.
  • the reaction can be described by the following equations summarizing desorption, reduction, and H2 synthesis / C12 recycling:
  • Such an embodiment is indicated, for example, when the H2 synthesis plant is designed such that chlorine is produced as a by-product.
  • C02 release may be physico-chemical in a pressure reduction ("degassing") plant
  • degassing pressure reduction
  • Such degasification plants are known per se
  • the advantage of this embodiment is that a technically simple and robust plant is provided Embodiment is particularly advantageous if in the C02 absorption plant a wash liquor was used, which enters into a predominantly physical bond or weak chemical bond with the CO 2, ie essentially absorptive or coordinative effects occur.
  • H2 - synthesis plant (module d): The supply of the required hydrogen can be based on electrochemical mixing (module dl) and / or solar thermal (module d2) path, wherein electrochemical H2 - synthesis systems are preferred.
  • electrochemical H2 - synthesis systems are preferred.
  • electrochemical cells are suitable which electrolyze aqueous solutions to form hydrogen.
  • Such cells are known, extensively studied and can be designed by the skilled person and integrated into the overall process.
  • An adaptation is meaningful or necessary, for example, to the previous C02 desorption plant.
  • all known solar thermal processes are suitable which lead to H2 release. Again, an adaptation to the other systems makes sense or necessary.
  • operational reliability, investment costs and efficiency are important parameters in all H2 synthesis plants.
  • Module dl In an advantageous embodiment, the H2 production takes place by means of PEM electrolysis (proton exchange membrane). This technology is state of the art and can be easily implemented on the required scale.
  • the H2 production takes place by means of chlorine-alkali electrolysis of an aqueous saline solution.
  • all known electrolysis cells are suitable. This embodiment is particularly advantageous when CO 2 desorption is by chlorination.
  • the H2 production takes place by means of high-temperature electrolysis of water to form hydrogen and oxygen.
  • water in principle, all known electrolysis cells are suitable.
  • the water used is first desalted, for example by means of ion exchange or distillation. This embodiment is particularly advantageous when CO 2 desorption is not achieved by chlorination.
  • the aqueous formed in the CO 2 absorption Carbonate / bicarbonate solution fed directly to an electrolysis, with CO2 and 02 is formed at the anode and H2 at the cathode and a hydroxide-containing solution is formed, which can be recycled for CO2 absorption ("low pressure alkaline electrolysis")
  • Electrolysis cells are known per se and described in US3135673, the contents of which are incorporated by reference into this specification. In essence, the reaction can be described by the following equation:
  • this electrolysis cell can be constructed so that in a three-part, separated by diaphragms cell H2 and 02 can be removed at the cathode or anode chambers and the C02 formed can be removed in the intermediate region.
  • the required hydrogen is produced by solar thermal processes without electricity. This can be done for example by thermal dissociation of ZnO at temperatures above 2000 K where Zn and * s 02 are formed. Zn reacts with H2O to form ZnO releasing H2.
  • This embodiment is advantageous when solar radiation is available in high intensity.
  • Such a solar thermal H2 synthesis plant may advantageously be combined with a CO 2 desorption plant which releases the CO 2 due to thermal processes, as described above.
  • the reaction energy required for all endothermic processes can be made available thermally. Thermal energy is provided for CO 2 desorption and H2 synthesis; The CO2 absorption and the synthesis of methanol, DME, methane are exothermic reactions.
  • the particular advantage of this embodiment would therefore be the low demand for electrical energy and the high Overall efficiency of the power plant to see. Accordingly, such a power plant in regions with high solar radiation, eg. In desert regions, would be advantageous to install.
  • Synthesis plant for the production of combustible hydrocarbons (module e).
  • the synthesis of combustible hydrocarbons, especially methanol, methane, DME, as well as corresponding plants are known in the art.
  • systems are used which are based on catalytic synthesis processes.
  • Methanol Synthesis Plant (Module el): As already stated, the present invention encompasses methanol synthesis plants which either i)
  • Transfer methanol can be designed so that, with a simple throughput, virtually complete conversion to methanol takes place.
  • these systems can also be designed or operated in such a way that only partial conversion of the CO or CO2 used takes place.
  • unreacted starting material is recycled either after removal of the product (methanol). or (especially in the case of CO2) released into the environment.
  • a complete (or virtually complete) recycling takes place without release to the environment.
  • the methanol synthesis is carried out from the components CO2 and H2.
  • Equipment for the conversion of C02 and H2 to methanol are well known. Typically, these plants are designed so that in the reactor, the reaction at 50 - 100 bar, 200 - 300 0 C takes place.
  • the reactors can be designed as fixed bed or fluidized bed reactors. Suitable catalysts are, for example, Cu-doped solids. material catalysts.
  • the methanol synthesis can be carried out in one or more stages. This reaction can be illustrated by the following reaction equation:
  • a distillation unit is provided in this plant, which allows the partial or complete separation of the water formed from methanol.
  • the invention thus also relates to a power plant as described herein, in which the methanol synthesis plant contains a C-containing catalyst (for the conversion of CO2 and H2), and optionally a distillation unit (for partial or complete separation of the methanol produced and for the return of the water for electrolysis) is assigned.
  • the methanol / synthesis gas plant contains a unit for the high-temperature electrolysis of CO2.
  • such units contain an oxygen ion-conducting solid electrolyte, for example ZrO / Y 2 O 3. Typical reaction temperatures are about 800 - 1000 0 C.
  • the unit supplied CO2 / H2O - mixtures are reduced upon application of a voltage in accordance with the following equations: C02 -> CO + H20 1/202 -> 2H2 + 02.
  • the stoichiometry of the synthesis gas produced depends on the applied voltage, the contact time, the residence time, the temperature and can be optimized in simple series experiments. If such a high-temperature electrolysis is combined with the methanol / synthesis gas plant, depending on the operating point of the high-temperature electrolysis unit, a separate H2 synthesis plant can be dispensed with.
  • the methanol / synthesis gas plant is combined with a plant for reductive alkaline low pressure electrolysis. This system provides the required CO.
  • the methanol synthesis is carried out according to:
  • This plant is referred to as a "direct methanol plant.” This process is particularly advantageous since the components CO2 and H2O can be used directly, and in this variant, the methanol and hydrogen synthesis plant (plants d) and e)) are in Such systems are known per se and eg in US 5928806, the contents of which are incorporated by reference into this specification.
  • Methane synthesis plant (module e2): In one embodiment, the methane synthesis takes place from the Components C02 and H2. Facilities for the conversion of CO2 and H2 to methane are well known. Typically, these systems are designed so that in the reactor, the reaction at 1 - 30 bar, preferably at atmospheric pressure, 300 - 400 0 C takes place.
  • the reactors can be designed as fixed bed or fluidized bed reactors. Suitable catalysts are, for example, Ni-doped solid catalysts.
  • the methanol synthesis can be carried out in one or more stages, preferably in one stage. This reaction can be illustrated by the following reaction equation:
  • This variant is particularly advantageous because it can be easily miniaturized, that non-pressure process variants are already known and that can be dispensed with a distillative purification. These advantages can override the disadvantage of storing under pressure partially or completely.
  • the invention thus also relates to a power plant as described here, in which the methane synthesis plant contains a Ni-containing catalyst (for the conversion of CO2 and H2), and to which no distillation unit for product separation is assigned.
  • the DME synthesis is from methanol with elimination of water. Facilities for this implementation are well known. Typically, these systems are designed so that the reaction takes place in the reactor at 30-80 bar, preferably at 50 bar, 200-300 0 C.
  • the reactors can be designed as fixed bed or fluidized bed reactors. Suitable catalysts are, for example, Cu / Fe-doped solid catalysts. This variant is particularly advantageous since DME generates an energy carrier which can be liquefied under low pressure.
  • the DME synthesis can be done directly; corresponding systems and catalysts are known. The gross equations of such reactions are given below: 3CO + 3H2 -> H3C-O-CH3 + C02
  • Storage System (Module f): Storage systems for liquid or gaseous combustible hydrocarbons are known per se.
  • Methanol Storage System (Module fl): Storage tanks ("tanks") suitable for methanol are known per se and because of their physicochemical properties, in particular flash point, vapor pressure and solution properties, tanks must be made of suitable materials and have appropriate safety features
  • the invention also relates to a floating body as described herein, consisting of two separate, interconnected devices in which the one device only Appendix f) contains and the second device includes the systems a) - e).
  • Methane storage facility (module f2): Methane storage facilities are preferably designed to handle either gaseous methane at 200bar (“CNG”) at ambient temperature or gaseous methane without pressure and at ambient temperature or liquid methane and depressurised at -163 ° C (. LNG NV) is stored corresponding systems are already industrially deployed Moreover, the statements made for methanol DME apply accordingly - storage installation (module f3):.... the statements made for methanol make correspondingly for DME DME is similar to LPG saved, so that the corresponding plants can be used according to this invention. DME storage systems are preferably designed so that the liquid DME is stored at 5 bar and ambient temperature.
  • the present invention therefore also relates to a watercraft as described herein, consisting of a composite of two or more individual vessels, characterized in that a first vessel contains the plants a) - e) and the associated further vessels each one Storage facility f) included.
  • a first vessel contains the plants a) - e) and the associated further vessels each one Storage facility f) included.
  • the methanol storage plant is separated by a movable partition wall (for example a membrane) into two partial volumes. So it is possible to store in the system water, which is needed in the course of the reaction.
  • the volume of water consumed corresponds approximately to the volume of methanol formed. This measure makes it possible to dispense with a local water supply system.
  • this embodiment leads to increased stability.
  • the floating body may contain other equipment ("ancillary equipment” or modules), including equipment used to purify starting materials, to supply and recover auxiliary materials and to recover energy, in particular thermal energy It is also possible to provide temporary storage for the intermediately formed products, for example batteries for intermediate storage electrical energy, gas tanks for the intermediate storage of CO2, and H2. Liquid tanks for temporary storage of auxiliaries. It is also possible to provide plants for regenerating the catalysts and the electrolysis cells. Furthermore, it is possible to provide storage for the optionally generated oxygen. These auxiliary systems are known per se and can be designed accordingly by the person skilled in the art.
  • the scaling of a power plant according to the invention depends on various parameters and is not limited by the invention.
  • the available wind or solar energy and the plants known therefor typically represent an upper limit.
  • To characterize the size of the power plant according to the invention it is possible to specify the primarily generated electrical energy (by wind or solar energy), since the other plants are tuned to it become. For large systems, for example, a single wind power plant with approx. 10 MW would have to be mentioned as an upper power limit. On this performance, the other components are interpreted.
  • the size of the systems d) to e) represents a lower limit, because below a critical size, the systems are too small for efficient operation. In connection with a direct methanol fuel cell, about 100 W would be mentioned as the lower power limit.
  • the invention relates to a kartebundenes power plant with a power of 100 W to 10 MW, preferably from 1 kW to 5 MW power, more preferably from 0.5 to 3 MW power.
  • the invention also relates to a power plant which preferably in places with constant wind conditions or suitable currents of the water or suitable wave movements of the water (such described below).
  • This positioning solves many of the problems of existing wind turbines (for land-based installations: especially noise, landscape), for offshore installations: especially costs for foundations, maintenance and network connection) or hydroelectric power plants.
  • the present invention relates to a floating body, in particular a watercraft, comprising the following installations: a) wind power plant or hydroelectric power plant for generating electrical energy for the operation of the facilities b) to f); b) CO2 absorption system for the absorption of atmospheric CO2; c) CO2 desorption plant for the desorption of the CO2 obtained in b); d) electrochemical H2 synthesis plant; e) catalytic synthesis plant for the production of combustible hydrocarbons; f) storage facility for storing the hydrocarbons obtained in e).
  • Such a floating body offers the possibility of producing and storing combustible hydrocarbons (such as methane, DME or methanol) from the virtually unlimited resources CO2 of the air and H2 of the water by means of wind energy or hydropower. Since all necessary resources are available free of charge, it is thus possible to economically produce these combustible hydrocarbons as a valuable and environmentally neutral energy source. Furthermore, the storage of such hydrocarbons is possible on such a device.
  • the individual plant parts a) to f) are known per se and can be dimensioned on the basis of general knowledge and adapted to the requirements in the operation of a floating device.
  • the systems a) to f) are preferably designed as described in this document.
  • buoyant can be installed remotely from the consumer as there are no loss of power due to transmission or network connection costs, which can be avoided, for example. an intercontinental transport of energy even from an economic point of view.
  • a basic idea of the present invention is therefore to "harvest" regenerative energy where it is obtained uniformly and in high density, to convert this energy obtained into a chemical energy carrier which is stored and emptied discontinuously for further use.
  • such a float can be easily repositioned; For example, to perform maintenance or to operate in regions with optimal wind / wave / flow conditions.
  • the invention therefore relates to a watercraft as a floating body, which is equipped with a WKA.
  • the axial resistance of the rotor can be used for the propulsion of the float so as to enable or assist the positioning / re-positioning.
  • the invention therefore relates to a buoy as a floating body, which is equipped with a WKA.
  • the invention therefore relates to a sailboat as a floating body, which is equipped with a water turbine.
  • the present invention relates to the use of a non-powered power plant or a floating body as described herein, in particular a buoy or a watercraft, for the production and storage of combustible hydrocarbons such as methanol methane, DME,.
  • the power plant is designed so that the essential or exclusive purpose is the production and (intermediate) storage of combustible hydrocarbons.
  • the floating body may be designed so that its essential or exclusive intended purpose is the production and the
  • Auxiliary units are used to drive the float or that the generated hydrocarbon is used in other processes. It is preferred to use the floating body according to the invention for the production and storage of combustible hydrocarbons, in particular methane or methanol or DME.
  • the invention in a fourth aspect, relates to a process for producing combustible hydrocarbons (in particular methanol, methane and / or DME) comprising the steps of a) positioning a power plant or a floating body as described here in a region which constant wind conditions, constant wave motion or constant Having solar radiation; b) operation of the facilities of this power plant / float; c) discontinuous, preferably periodic, emptying of the storage facility.
  • This method makes it possible to produce a chemical energy carrier in a simple and safe manner as well flexible and needs-oriented. The individual steps are explained below.
  • Step a) Regions with constant wind conditions are well known; The necessary strength of the wind depends on the design of the wind turbine. Typically, an average wind speed of at least 7m / s should be present. Wind conditions are considered constant when the average wind speed is at least 70%, preferably at least 80% of the time. Typical regions are the areas of the trade winds and areas that form a "natural nozzle" (such as coastal areas, areas between islands, mountain passes, summits, etc.) Generally, positioning should take into account that constant wind increases the degree of utilization; low wind shear reduces wear and also increases performance, and in particular trade winds meet these requirements, which is a significant advantage over land-based installations.
  • Regions of constant wave motion are well known; The necessary strength of the waves depends on the design of the wave power plant. Typically, waves with a height of ⁇ 10 m, for example 2-8 m should be present. Shaft ratios are considered constant when the average annual wave height is more than 0.7 m. Typical regions are the areas of the South Pacific.
  • Regions of constant solar radiation are also well known. Suitable areas are those in which the average intensity of solar radiation averages more than 200 watts / m2 per year. Typical areas are, for example, on the Arabian Peninsula or in northern Africa.
  • the positioning of the vessel can be done in several ways. In the simplest case, the vessel is anchored to the desired position. Alternatively, the vessel may cruise in the wind, being kept on course by engine power and / or wind power, depending on the design. In a further alternative, the vessel is re-positioned at certain intervals, for example, in changing weather conditions or due to seasonal fluctuations.
  • the invention therefore also relates to a method in which the positioning of the floating body optionally comprises a continuous or discontinuous repositioning.
  • the resistance of the wind turbine for driving the float in particular a ship, can be partially or completely used.
  • the invention therefore also relates to a method as described herein, in which the positioning and / or re-positioning of the floating device takes place with partial or complete utilization of the resistance of the wind turbine.
  • the positioning of a power plant which is not installed on a float essentially relates to the advantageous installation of the wind turbine or solar thermal system, whereby the criteria mentioned here are applicable.
  • Step b) The operation of the individual systems is carried out according to the interpretation in a known manner.
  • the individual plant components must be coordinated in their production capacity.
  • the generated electrical energy must be sufficient for all parts of the plant b) to f) as well as any ancillary components which may be present. be coordinated by H2 and the desorption of CO2.
  • the equipment may be designed to allow for fully automatic, remote-controlled production, or for an on-site operator team, as well as combinations thereof. If the vessel is at anchor, fully automated operation is possible. If the vessel crosses in the wind, at least a partial manual operation is preferred, which monitors and controls at least the positioning of the vessel.
  • Step c) the emptying of the storage facility takes place discontinuously, preferably in periodic periods.
  • the parameters for this can be either a time unit (eg monthly, quarterly, yearly) or the level of the storage facility (eg at least 50% filled, maximum 90% filled), or a spatial parameter (eg a vessel cruising in the trade wind driving a certain course), or a combination thereof.
  • a time unit eg monthly, quarterly, yearly
  • the level of the storage facility eg at least 50% filled, maximum 90% filled
  • a spatial parameter eg a vessel cruising in the trade wind driving a certain course
  • a float is equipped with the following equipment:
  • a tank for holding the methanol formed as module f, volume 300m3.
  • This power plant produces 50 kg of methanol / h, which corresponds to an energy content Hu of 274 kWh (efficiency 46%).
  • the components caustic soda and
  • Example 2 Wind power plant A power plant with the following plants
  • Such a power plant can, for example, on a
  • a sailing ship is equipped with the following facilities
  • Such a ship can, for example, be operated cruising in the trade wind.
  • Example 4 purely thermal power plant A power plant with the following modules
  • Such a power plant can be installed, for example, on the Arabian Peninsula.
  • a gas engine is provided, which uses the methane produced as fuel.
  • a module a is necessary in this embodiment only for the supply of auxiliary equipment.
  • a ship is equipped with the modules b) to f) described below, several modules a) are connected to it
  • Such a power plant can be installed, for example, in the south pacific.

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Abstract

L'invention concerne une centrale électrique indépendante du réseau, qui contient les installations suivantes, dont les capacités sont coordonnées : a) installation éolienne, installation hydroélectrique, installation solaire et/ou installation photovoltaïque pour la production d'énergie électrique pour le fonctionnement des installations b) à f) ; b) installation d'absorption de CO2 pour l'absorption de CO2 atmosphérique ; c) installation de désorption de CO2 pour la désorption du CO2 obtenu en b) ; d) installation électrochimique ou solaire de synthèse d'H2, pour le fonctionnement de l'installation e) ; e) installation de synthèse sélectionnée parmi le groupe comprenant la synthèse catalytique du méthanol, la synthèse catalytique du DME et la synthèse catalytique du méthane ; f) installation de stockage sélectionnée parmi le groupe comprenant les installations de stockage de méthanol, les installations de stockage de DME et les installations de stockage de méthane. L'invention concerne en outre l'utilisation d'une telle centrale électrique, et un procédé pour faire fonctionner une telle centrale électrique.
PCT/EP2008/009803 2007-11-22 2008-11-20 Centrale électrique modulaire, indépendante du réseau WO2009065577A1 (fr)

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US12/744,104 US8715581B2 (en) 2007-11-22 2008-11-20 Modular power plant unconnected to the grid
AT08851992T ATE537358T1 (de) 2007-11-22 2008-11-20 Modulares, netzungebundenes kraftwerk
EP08851992A EP2220367B1 (fr) 2007-11-22 2008-11-20 Centrale électrique modulaire, indépendante du réseau

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010041329A1 (de) * 2010-09-24 2012-03-29 Siemens Aktiengesellschaft Vorrichtung zur Erwärmung von Erdreich
WO2013029701A1 (fr) * 2011-08-29 2013-03-07 Ostsee Maritime Gmbh Installation d'alimentation en énergie, destinée notamment au domaine des technologies domestiques
DE102011088313A1 (de) 2011-12-12 2013-06-13 Wobben Properties Gmbh Verfahren zum Betrieb einer Windenergieanlage bzw. eines Windparks
EP2607303A1 (fr) 2011-12-22 2013-06-26 Friedrich-Alexander-Universität Erlangen-Nürnberg Procédé d'emmagasinage d'énergie se présentant sous la forme d'énergie électrique ou de chaleur dans un mélange gazeux d'éduit ainsi qu'un dispositif d'exécution de ce procédé
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WO2019197975A1 (fr) 2018-04-09 2019-10-17 Kiss Zoltan J Chauffage solaire à l'air avec co2 intégré à partir d'un système d'absorption d'air
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* Cited by examiner, † Cited by third party
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EP2928852A4 (fr) * 2012-12-05 2017-01-04 Cri Ehf Système et procédé pour capturer des émissions industrielles et recyclage pour la production de produits chimiques
EA024944B1 (ru) * 2012-12-26 2016-11-30 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Иркутская государственная сельскохозяйственная академия" Водородная установка для использования энергии восполняемых источников с сезонно-цикловым режимом энергопотребления
DE102014112580B4 (de) * 2014-09-01 2019-01-24 Mitsubishi Hitachi Power Systems Europe Gmbh Industrielle Produktionsanlage mit minimalem Treibhausgasausstoß, insbesondere Kohlendioxidausstoß, und Verfahren zum Betrieb desselben
US9914644B1 (en) 2015-06-11 2018-03-13 X Development Llc Energy efficient method for stripping CO2 from seawater
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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4085795A (en) * 1976-05-10 1978-04-25 George Herbert Gill Method for using geothermal energy
US4339547A (en) 1979-09-21 1982-07-13 Grumman Aerospace Corporation Production of synthetic hydrocarbons from air, water and low cost electrical power
US4627418A (en) * 1980-09-08 1986-12-09 Geruldine Gibson Apparatus for the carbothermic reduction of metal oxides using solar energy
DE3933284A1 (de) * 1989-10-05 1991-04-18 Steinmueller Gmbh L & C Verfahren zur kontinuierlichen erzeugung elektrischer energie aus solarenergie und solarkraftwerk zur durchfuehrung des verfahrens
DE4332789A1 (de) * 1993-09-27 1995-03-30 Abb Research Ltd Verfahren zur Speicherung von Energie
DE19802660A1 (de) 1998-01-24 1999-07-29 Goes Ges Fuer Forschung Und Te Abprodukt-Wärmekraft-Synthese-Kopplung, ein Verfahren zur regionalen Be- und Entsorgung
WO2000025380A2 (fr) 1998-10-27 2000-05-04 Quadrise Limited Stockage d'energie electrique
WO2005056737A1 (fr) 2003-12-13 2005-06-23 SCHRÖDER, Sascha Procede et installation de production de porteurs d'energie fluides a partir d'un porteur d'energie solide
US20050232833A1 (en) 2004-04-15 2005-10-20 Hardy Dennis R Process for producing synthetic liquid hydrocarbon fuels
WO2007058608A1 (fr) 2005-10-14 2007-05-24 Morphic Technologies Ab (Publ) Procede et systeme de production, de conversion et de stockage d'energie

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3852180A (en) * 1972-02-04 1974-12-03 Skf Ind Trading & Dev Apparatus for co{11 {11 conversion to methane
US4341069A (en) * 1980-04-02 1982-07-27 Mobil Oil Corporation Method for generating power upon demand
US5246551A (en) 1992-02-11 1993-09-21 Chemetics International Company Ltd. Electrochemical methods for production of alkali metal hydroxides without the co-production of chlorine
DE4235125C2 (de) 1992-10-17 1994-09-29 Zsw Verfahren zur Herstellung von Synthesegas und Vorrichtung zum Durchführen des Verfahrens
DE19522215C2 (de) * 1995-06-20 1999-12-02 Nikolaus Laing Schwimmendes Solarkraftwerk und Verfahren zu seinem Betrieb
ATE441030T1 (de) * 2002-03-08 2009-09-15 Ocean Wind Energy Systems Offshore-windenergieanlage
US7318854B2 (en) * 2004-10-29 2008-01-15 New Jersey Institute Of Technology System and method for selective separation of gaseous mixtures using hollow fibers
AU2007276694A1 (en) * 2006-07-17 2008-01-24 Commonwealth Scientific And Industrial Research Organisation CO2 capture using solar thermal energy
US20100205856A1 (en) 2007-10-11 2010-08-19 Los Alamos National Security Llc Method of producing synthetic fuels and organic chemicals from atmospheric carbon dioxide

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4085795A (en) * 1976-05-10 1978-04-25 George Herbert Gill Method for using geothermal energy
US4339547A (en) 1979-09-21 1982-07-13 Grumman Aerospace Corporation Production of synthetic hydrocarbons from air, water and low cost electrical power
US4627418A (en) * 1980-09-08 1986-12-09 Geruldine Gibson Apparatus for the carbothermic reduction of metal oxides using solar energy
DE3933284A1 (de) * 1989-10-05 1991-04-18 Steinmueller Gmbh L & C Verfahren zur kontinuierlichen erzeugung elektrischer energie aus solarenergie und solarkraftwerk zur durchfuehrung des verfahrens
DE4332789A1 (de) * 1993-09-27 1995-03-30 Abb Research Ltd Verfahren zur Speicherung von Energie
DE19802660A1 (de) 1998-01-24 1999-07-29 Goes Ges Fuer Forschung Und Te Abprodukt-Wärmekraft-Synthese-Kopplung, ein Verfahren zur regionalen Be- und Entsorgung
WO2000025380A2 (fr) 1998-10-27 2000-05-04 Quadrise Limited Stockage d'energie electrique
WO2005056737A1 (fr) 2003-12-13 2005-06-23 SCHRÖDER, Sascha Procede et installation de production de porteurs d'energie fluides a partir d'un porteur d'energie solide
US20050232833A1 (en) 2004-04-15 2005-10-20 Hardy Dennis R Process for producing synthetic liquid hydrocarbon fuels
WO2007058608A1 (fr) 2005-10-14 2007-05-24 Morphic Technologies Ab (Publ) Procede et systeme de production, de conversion et de stockage d'energie

Cited By (18)

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DE102011088313A1 (de) 2011-12-12 2013-06-13 Wobben Properties Gmbh Verfahren zum Betrieb einer Windenergieanlage bzw. eines Windparks
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US9541067B2 (en) 2011-12-12 2017-01-10 Wobben Properties Gmbh Method for operating a wind turbine or a wind farm
EP2607303A1 (fr) 2011-12-22 2013-06-26 Friedrich-Alexander-Universität Erlangen-Nürnberg Procédé d'emmagasinage d'énergie se présentant sous la forme d'énergie électrique ou de chaleur dans un mélange gazeux d'éduit ainsi qu'un dispositif d'exécution de ce procédé
DE102011089656A1 (de) 2011-12-22 2013-06-27 Friedrich-Alexander-Universität Erlangen-Nürnberg Verfahren zur Einspeicherung von Energie die in Form von elektrischem Strom oder Wärme vorliegt in ein Eduktgasgemisch sowie eine Vorrichtung zur Durchführung dieses Verfahrens
EP3968483A1 (fr) 2012-03-02 2022-03-16 Wobben Properties GmbH Procédé permettant de faire fonctionner une centrale électrique combinée et centrale électrique combinée
DE102012203334A1 (de) 2012-03-02 2013-09-05 Wobben Properties Gmbh Verfahren zum Betreiben eines Kombikraftwerks bzw. Kombikraftwerk
WO2013128023A2 (fr) 2012-03-02 2013-09-06 Wobben Properties Gmbh Procédé permettant de faire fonctionner une centrale électrique combinée et centrale électrique combinée
JP2015513890A (ja) * 2012-03-02 2015-05-14 ヴォッベン プロパティーズ ゲーエムベーハーＷｏｂｂｅｎ Ｐｒｏｐｅｒｔｉｅｓ Ｇｍｂｈ コンビネーション発電所を稼働するための方法、並びにコンビネーション発電所
DE102013001403A1 (de) * 2013-01-28 2014-07-31 Etogas Gmbh Verfahren und Anlage zur Herstellung eines chemischen Produkts
DE102017222948A1 (de) * 2017-12-15 2019-01-24 Thyssenkrupp Ag Produktion von Ammoniak und Wasserstoff mit direkter Stromeinspeisung aus Offshore Energiegewinnungsanlagen
WO2019197975A1 (fr) 2018-04-09 2019-10-17 Kiss Zoltan J Chauffage solaire à l'air avec co2 intégré à partir d'un système d'absorption d'air
US10617998B2 (en) 2018-04-09 2020-04-14 Zoltan J. Kiss Methods to extract carbon dioxide from the atmosphere using a solar PV module as part of a combined cycle energy converter
DE102020129374A1 (de) 2020-11-07 2022-05-12 Obrist Technologies Gmbh Anlage und Verfahren zur Herstellung eines global nutzbaren Energieträgers
CN117869186A (zh) * 2024-01-10 2024-04-12 东北电力大学 一种压缩二氧化碳储能与合成二甲醚的海上综合能源系统
CN117869186B (zh) * 2024-01-10 2024-05-28 东北电力大学 一种压缩二氧化碳储能与合成二甲醚的海上综合能源系统

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US8715581B2 (en) 2014-05-06

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